Technical and Cost Assessment of Electrocatalytic Bromate Removal from Drinking Water

被引:0
|
作者
Lee, Kuan-Lin [1 ]
Yan, Chenxu [1 ,2 ]
Xu, Jingwen [1 ]
Brady, Carolyn E. [3 ]
Werth, Charles J. [1 ]
机构
[1] Univ Texas Austin, Maseeh Dept Civil Architectural & Environm Engn, Austin, TX 78712 USA
[2] Carollo Engineers Inc, Austin, TX 78759 USA
[3] Univ Austin Texas, Dept Chem, Austin, TX 78712 USA
来源
ACS ES&T ENGINEERING | 2024年 / 4卷 / 09期
基金
美国国家科学基金会;
关键词
electrocatalytic reduction; bromate; palladium; cathode regeneration; cost assessment; ELECTROCHEMICAL REDUCTION; BIMETALLIC CATALYST; CARBON; ELECTRODE; OXIDATION; KINETICS; HYDROGEN; COADSORPTION; SULFUR; IMPACT;
D O I
10.1021/acsestengg.4c00203
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Bromate is a potential human carcinogen and is commonly found in water and wastewater after ozonation. Electrocatalytically, Pd has shown good activity in reducing bromate to bromide; however, the energy efficiency and cost of this technology in a realistic treatment system remain unknown. A custom filter-press reactor with minimal mass-transfer limitations was used to test the kinetics and energy consumption for bromate reduction using Pd, Ru, or Cu on activated carbon cloth as the cathode. In phosphate-buffered nanopure water at circumneutral pH, 95% of bromate was reduced to bromide (from 200 to 10 mu g/L) in 1 h with a normalized activity of 2136 mL min(-1) g(Pd)(-1). The total energy consumption was 0.576 kW h per gram of bromate removed, which is 9 to 43 times lower than that in reported studies. In Austin tap water (TW) at pH 9.5, the normalized activity dropped to 544 mL min(-1) g(Pd)(-1), and the total energy consumption increased to 2.198 kW h per gram of bromate removed, still an improvement over all values reported in the literature despite the latter using synthetic waters. This superior performance is due to the design of the filter-press reactor that minimizes mass-transfer limitations as well as solution resistance compared to reactors evaluated in the literature, such as batch and three-dimensional electrochemical reactors. We note that any lost activity due to catalyst oxidation and poisonings in TW can be electrochemically regenerated by briefly applying a positive and strongly negative potential. This electrocatalytic treatment has estimated costs of $1.41 per 1000 gal (91% capital costs and 9% O&M costs) and is comparable to ion exchange, granular activated carbon, and reverse osmosis, yet benefits from no waste stream generation, indicating that this technology is ready for evaluation at the pilot scale.
引用
收藏
页码:2186 / 2197
页数:12
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